CN206089117U - A coalescence drum reactor for sewage treatment - Google Patents

A coalescence drum reactor for sewage treatment Download PDF

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Publication number
CN206089117U
CN206089117U CN201621133809.2U CN201621133809U CN206089117U CN 206089117 U CN206089117 U CN 206089117U CN 201621133809 U CN201621133809 U CN 201621133809U CN 206089117 U CN206089117 U CN 206089117U
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CN
China
Prior art keywords
coalescence
swash plate
oil
area
hydroecium
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Expired - Fee Related
Application number
CN201621133809.2U
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Chinese (zh)
Inventor
左昌平
李梅英
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Xinjiang Link Environmental Engineering Co Ltd
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Xinjiang Link Environmental Engineering Co Ltd
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Priority to CN201621133809.2U priority Critical patent/CN206089117U/en
Application granted granted Critical
Publication of CN206089117U publication Critical patent/CN206089117U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model discloses a coalescence drum reactor for sewage treatment, including settling cask, inlet tube, coarse grain granule, high -velocity jet water injection well choke, swash plate, receipts bagger, oil collecting chamber, oil -out, communicating pipe, floater, overflow pipe, delivery port. This a coalescence drum reactor for sewage treatment has solved the miniaturized problem of equipment of carrying out water oil separating to the thin oil, has reduced the processing load of subsequent processing equipment, has shortened the oily sewage settling time, and efficient, installation convenient to use is fit for little oil field sewage precise monitoring and recycle, has practiced thrift a large amount of water sources.

Description

A kind of coalescence barrel reactor for sewage disposal
Technical field
The utility model is related to a kind of field of sewage treatment, more particularly to a kind of coalescence cylinder for sewage disposal Reactor.
Background technology
With the growth of countries in the world industrial expansion and urban population, a large amount of industry of discharge and sanitary sewages, seriously Water body is polluted, the ecological balance is destroyed.In recent decades each state all takes control measures, so as to industry and sanitary sewage Pollution problem hexyl is originally resolved.China grabs in each oil field to efforts at environmental protection must compare early, but because a variety of causes is until nearly ten In the past few years just start to pay attention to.
Oil field at home is the needs for increasing production stable yields, carries out rolling development, construction cycle at main force oil field edge mostly at present Short, existing Produced Liquid majority is pulled to multi-purpose station by automobile carries out processed or local dewatered rear wastewater disposition, the former production cost Height, the latter causes environmental pollution.And such small oil field mostly is waterflooding extraction, need to carry out re-injection with clear water, both wasted water Resource, increases operating cost again.With increasing for crude oil water containing, some small oil fields are transported to multi-purpose station and are processed using pipe, The sewage disposal burden of multi-purpose station is increased again, causes to be arranged outside part of contaminated water, cause environmental pollution.
Oil field at home be particularly Henan Oil neoasozin canopy, Zhang Dian, Dong Zhuan, Wang Ji, western part this Butut Deng You areas just will face with Upper problem.Solving the problem must just go up sewage-treatment plant, realize sewage re-injection on the spot.The large-scale multi-purpose station mesh of oil field at home Front sewage disposal system typically using two-stage gravitational settling and double-filtration flow process, processing equipment because efficiency is low, volume big, Investment is high, and for fault-block oilfield, the rolling development cycle is shorter, builds that fixed sewage-treatment plant is costly, floor space is big, Equipment scrapping after the transfer of oil field, it is very uneconomical in operation.
The content of the invention
In order to solve the above problems;The utility model provides a kind of coalescence barrel reactor for sewage disposal, the use Solve the problems, such as to carry out thin oil the device miniaturization of water-oil separating in the coalescence barrel reactor of sewage disposal, reduce follow-up The process load of processing equipment, shortens the oil-polluted water sedimentation time;And efficiency high, easy to install, suitable small oil field dirt Water treatment in situ and re-injection, have saved substantial amounts of water source.
The utility model solves the technical scheme that its technical problem adopted:A kind of coalescence cylinder for sewage disposal Reactor, including settling tank, water inlet pipe, at a high speed coarse particle, injection water nozzle, swash plate, receipts bucket, gathering room, oil-out, company Siphunculus, ball float, overflow pipe, delivery port;The settling tank be divided into entrance surge chamber, coarse section area, laterally stream inclined plate sedimentation area, Free settling area, the part of hydroecium six, entrance surge chamber left side is connected with water inlet pipe;Coarse is filled with coarse section area Grain;Swash plate is laterally installed, top is provided with injection water nozzle at a high speed, and bottom is installed and receives bucket in stream inclined plate sedimentation area;Free settling Separating in area has gathering room, and gathering room bottom is provided with oil-out;Hydroecium is set by connecting with free settling area communicating pipe in hydroecium Ball float is equipped with, top is provided with overflow pipe, and lower end is provided with delivery port.
Preferably, the high speed injection water nozzle is arranged on swash plate top, its water flow jet direction and swash plate incline direction one Cause;It is easy to the cleaning of swash plate.
Preferably, the swash plate is upper and lower two-layer staggered arrangement, and distance is 15~30mm between every layer of swash plate;It is effectively increased The worksheet area of separation equipment, reduces transport disengaging height, so as to improve the removal efficiency of oil droplet particle.
Preferably, control valve is installed on the hydroecium communicating pipe, by arranging its operation stroke, adjusts hydroecium communicating pipe Freeboard, so as to reach free settling room liquid level is adjusted, it is ensured that oil reservoir height, and can stably be flowed into grease chamber and discharged and set It is standby.
The utility model, a kind of coalescence barrel reactor for sewage disposal:Oil-polluted water is made by equipped with filler The device of (being also coarse particle), when sewage flows through filler, the process for making oil droplet and suspended solid change from small to big.Through Sewage after coarse, its oil content and sump oil property do not change, and are simply more readily available for settling tank gravitational separation process by dirt Oil and suspended solid are removed.Meanwhile, swash plate is added in settling tank, and free settling area is set, increase the work of separation equipment Surface area and settlement space, improve the removal efficiency of oil droplet particle and suspended solid.
The disposal ability of the settling tank is 1200m3/d, and sewage sinks in the time of staying of settling tank from the conventional big tank of tradition The drop time was reduced to 15 minutes by 6~12 hours.Settling tank is provided with sludge hopper and swash plate flusher and is provided with and surmounts flow process, After equipment operation a period of time, using settling tank flow process is surmounted, swash plate can be rinsed.Settling tank liquid level adopts glass tube liquid Position meter shows on the spot, and sets Floating Ball Liquid Level Control, and signal is delivered to into variable-frequency governor, is lifted by the control of settling tank liquid level signal Pump motor frequency control.
A kind of coalescence barrel reactor for sewage disposal of the utility model, its advantage is:
1) this is used for the coalescence barrel reactor of sewage disposal by coarse, inclined plate sedimentation, free settling, profit circle The several sewage disposal technology rhythm integrated uses such as face control, reach at utmost oil removing and suspended solid, reduce subsequent filter system System processes the purpose of load;
2) the coalescence barrel reactor for being used for sewage disposal processes oil-polluted water and shortens the sewage sedimentation time, reduces heavy Drop equipment volume;
3) this is used for sewage disposal coalescence barrel reactor small volume, efficiency high, occupation of land pound product, easy to install, Suitable small oil field sewage treatment in situ and re-injection;And the re-injection on the spot of small oil field sewage, not only can save substantial amounts of power supply, thermal source and Water source, and can make crude oil output pipeline not with constantly changing, direct economic benefit and potential because aqueous rising, liquid measure increase Benefit is very good.
Description of the drawings
The utility model is further illustrated with reference to the accompanying drawings and examples.
Fig. 1 is a kind of structural representation of the coalescence barrel reactor for sewage disposal of the utility model.
In figure, 1, settling tank, 2, entrance surge chamber, 3, coarse section area, 4, horizontal stream inclined plate sedimentation area, 5, free settling Area, 6, hydroecium, 11, water inlet pipe, 12, coarse particle, 13, injection water nozzle at a high speed, 14, swash plate, 15, receive bucket, 16, oil-collecting Room, 17, oil-out, 18, communicating pipe, 19, control valve, 20, ball float, 21, overflow pipe, 22, delivery port.
Specific embodiment
Refer to Fig. 1, this specific embodiment, including settling tank, water inlet pipe, at a high speed coarse particle, injection water nozzle, tiltedly Plate, receipts bucket, gathering room, oil-out, communicating pipe, ball float, overflow pipe, delivery port;The settling tank is divided into entrance surge chamber, thick Granulation sections area, laterally stream inclined plate sedimentation area, free settling area, the part of hydroecium six, entrance surge chamber left side is connected with water inlet pipe;Slightly Coarse particle is filled with granulation sections area;Swash plate is laterally installed, top is provided with injection water nozzle at a high speed in stream inclined plate sedimentation area, Install and receive bucket in bottom;Separating in free settling area has gathering room, and gathering room bottom is provided with oil-out;Hydroecium by communicating pipe with Free settling area connects, and ball float is provided with hydroecium, and top is provided with overflow pipe, and lower end is provided with delivery port.
Fig. 1 is refer to, the high speed injection water nozzle is arranged on swash plate top, its water flow jet direction and swash plate incline direction Unanimously;It is easy to the cleaning of swash plate.
Fig. 1 is refer to, the swash plate is upper and lower two-layer staggered arrangement, distance is 15~30mm between every layer of swash plate;Effectively Increase the worksheet area of separation equipment, transport disengaging height is reduced, so as to the removal efficiency of oil droplet particle can be improved.
Fig. 1 is refer to, control valve is installed on the hydroecium communicating pipe, by arranging its operation stroke, adjusted hydroecium and connect Siphunculus freeboard, so as to reach free settling room liquid level is adjusted, it is ensured that oil reservoir height, and can stably flow into grease chamber row Go out equipment.
Exemplary description is carried out to the utility model above in conjunction with accompanying drawing, it is clear that realization of the present utility model is not received The restriction of aforesaid way, as long as employing the various improvement that technical solutions of the utility model are carried out, or not improved says this practicality New design and technical scheme is applied to other occasions, in protection model of the present utility model.

Claims (4)

1. a kind of coalescence barrel reactor for sewage disposal, including settling tank, water inlet pipe, at a high speed coarse particle, injection Water nozzle, swash plate, receipts bucket, gathering room, oil-out, communicating pipe, ball float, overflow pipe, delivery port;It is characterized in that:The sedimentation Tank is divided into entrance surge chamber, laterally coarse section area, stream inclined plate sedimentation area, free settling area, the part of hydroecium six, entrance surge chamber Left side is connected with water inlet pipe;Coarse particle is filled with coarse section area;Laterally swash plate is installed in stream inclined plate sedimentation area, pushes up Portion is provided with injection water nozzle at a high speed, and bottom is installed and receives bucket;Separating in free settling area has gathering room, and gathering room bottom is provided with fuel-displaced Mouthful;Hydroecium is provided with ball float by connecting with free settling area communicating pipe in hydroecium, top is provided with overflow pipe, and lower end is provided with Delivery port.
2. a kind of coalescence barrel reactor for sewage disposal according to claim 1, it is characterised in that:The high speed Injection water nozzle is arranged on swash plate top, and its water flow jet direction is consistent with swash plate incline direction.
3. a kind of coalescence barrel reactor for sewage disposal according to claim 1, it is characterised in that:The swash plate For upper and lower two-layer staggered arrangement, distance is 15~30mm between every layer of swash plate.
4. a kind of coalescence barrel reactor for sewage disposal according to claim 1, it is characterised in that:The hydroecium Control valve is installed on communicating pipe.
CN201621133809.2U 2016-10-18 2016-10-18 A coalescence drum reactor for sewage treatment Expired - Fee Related CN206089117U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621133809.2U CN206089117U (en) 2016-10-18 2016-10-18 A coalescence drum reactor for sewage treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621133809.2U CN206089117U (en) 2016-10-18 2016-10-18 A coalescence drum reactor for sewage treatment

Publications (1)

Publication Number Publication Date
CN206089117U true CN206089117U (en) 2017-04-12

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CN201621133809.2U Expired - Fee Related CN206089117U (en) 2016-10-18 2016-10-18 A coalescence drum reactor for sewage treatment

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109019930A (en) * 2018-09-04 2018-12-18 江苏大洋环保工程有限公司 A kind of oily wastewater integrated high-efficiency processor

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109019930A (en) * 2018-09-04 2018-12-18 江苏大洋环保工程有限公司 A kind of oily wastewater integrated high-efficiency processor

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Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CB03 Change of inventor or designer information
CB03 Change of inventor or designer information

Inventor after: Zuo Changping

Inventor before: Zuo Changping

Inventor before: Li Meiying

CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20170412

Termination date: 20181018